WO2020168642A1 - Multi-kilogram-level knotless thread preparation process - Google Patents

Multi-kilogram-level knotless thread preparation process Download PDF

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Publication number
WO2020168642A1
WO2020168642A1 PCT/CN2019/087566 CN2019087566W WO2020168642A1 WO 2020168642 A1 WO2020168642 A1 WO 2020168642A1 CN 2019087566 W CN2019087566 W CN 2019087566W WO 2020168642 A1 WO2020168642 A1 WO 2020168642A1
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temperature
parts
cooling
drying
barrel
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PCT/CN2019/087566
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French (fr)
Chinese (zh)
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卢崇国
卢静
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海安县中祥线业有限公司
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    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01FCHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
    • D01F1/00General methods for the manufacture of artificial filaments or the like
    • D01F1/02Addition of substances to the spinning solution or to the melt
    • D01F1/10Other agents for modifying properties
    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01FCHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
    • D01F8/00Conjugated, i.e. bi- or multicomponent, artificial filaments or the like; Manufacture thereof
    • D01F8/04Conjugated, i.e. bi- or multicomponent, artificial filaments or the like; Manufacture thereof from synthetic polymers
    • D01F8/12Conjugated, i.e. bi- or multicomponent, artificial filaments or the like; Manufacture thereof from synthetic polymers with at least one polyamide as constituent
    • DTEXTILES; PAPER
    • D02YARNS; MECHANICAL FINISHING OF YARNS OR ROPES; WARPING OR BEAMING
    • D02GCRIMPING OR CURLING FIBRES, FILAMENTS, THREADS, OR YARNS; YARNS OR THREADS
    • D02G3/00Yarns or threads, e.g. fancy yarns; Processes or apparatus for the production thereof, not otherwise provided for
    • D02G3/02Yarns or threads characterised by the material or by the materials from which they are made
    • DTEXTILES; PAPER
    • D02YARNS; MECHANICAL FINISHING OF YARNS OR ROPES; WARPING OR BEAMING
    • D02GCRIMPING OR CURLING FIBRES, FILAMENTS, THREADS, OR YARNS; YARNS OR THREADS
    • D02G3/00Yarns or threads, e.g. fancy yarns; Processes or apparatus for the production thereof, not otherwise provided for
    • D02G3/44Yarns or threads characterised by the purpose for which they are designed

Definitions

  • the invention relates to the technical field of fiber processing, in particular to a multi-kilogram-level knotless thread preparation process.
  • the fishing line is the line that hangs on the fishing rod when fishing, similar to the silk spit out by a spider, very thin but very strong.
  • Fishing line is a kind of line commonly used in life. Fishing line is not only used for fishing, but we can also use tied things in our lives.
  • Nylon thread is also known as traditional thread, four-color thread.
  • the manufacturing process of nylon thread is generally made of resin processing and spinning (traditional thread) and adding other materials such as color (four-color thread) to the finished product. Its characteristic is that it has better ductility and elasticity.
  • nylon fishing line There are two basic specifications of nylon fishing line: one is the specifications set by European and American countries with "pounds", such as a ten-pound line, which can withstand a maximum tensile force of ten pounds; the other is a fishing line made in Japan. They are usually distinguished by "number” and specifications, and there are European ones.
  • the principle is the same as the concept of the number of pounds.
  • the maximum pulling force of a line of about one kilogram can be used as a standard basis for pulling fish in the water.
  • the thread based on nylon 6 monofilament is increasingly unable to meet people's comprehensive use in many fields, and there is still much room for improvement in performance.
  • the purpose of the present invention is to provide a multi-kilogram-level knotless thread preparation process, which adopts nylon 6 and nylon 66 materials in a certain ratio and is prepared with superior performance.
  • the present invention provides a multi-kilogram-level knotless preparation process, which includes the following steps:
  • the raw materials are mixed.
  • the raw materials include the following components by mass: 100 parts of nylon 6 chips, 100-150 parts of nylon 66 chips, 2-10 parts of compatibilizer, 20-50 parts of toughening agent, 0.8-1 parts of auxiliary Parts, 0.8-1 part of dispersant, mix the above raw materials;
  • the drying temperature is 110-125°C
  • the drying time is 3.5-4.5 hours
  • the drying vacuum degree is -0.07 ⁇ -0.09MPa
  • the moisture content of the slice is 750 -900ppm
  • the dried raw material is extruded and melted with a screw extruder and then spun, the spinning melt temperature is 180-220°C, and the temperature fluctuation of the spinning melt is controlled at ⁇ 2°C.
  • Pressure melting the temperature in the first zone is 190-200°C, the temperature in the second zone is 188-202°C, the temperature in the third zone is 190-205°C, and the temperature in the fourth zone is 185-199°C;
  • a side blowing device After spinning, a side blowing device is installed in the cooling tunnel for cooling.
  • the side blowing speed is 0.5 meters per second, the side blowing temperature is 19-27°C, and the wind humidity is 62-75%;
  • Oiling, spinning cluster oiling the concentration of the oiling agent is 12.8-14.4%, the oiling rate of the oiling agent: 0.75-0.95%, and the pressure regulating range is 0.32-2.1 kg;
  • the screw extruder includes a frame, an extrusion device is arranged on the frame, and a cooling device is arranged outside the extrusion device.
  • the extrusion device includes a barrel, a screw and an extrusion die, and a feed port is provided on the barrel.
  • the screw is arranged inside the barrel, the cooling device is arranged on the outside of the barrel, and the cooling device is a multi-section spiral cooling water channel wound on the outside of the barrel. The two ends of the cooling water channel are the water inlet and the water outlet respectively.
  • the outside of the extruder barrel is cooled in sections according to the internal partitions to ensure that the temperature of each partition meets the set requirements.
  • the spiral cooling water pipes provide uniform cooling and good results.
  • the flange temperature is 200-230°C
  • the box temperature is 190-205°C
  • the metering pump speed is 14-15 revolutions per minute.
  • the extrusion temperature is 210-240°C
  • the rotation speed is 200-260rpm
  • the temperature range of each zone of the extrusion process is 200-260°C
  • the residence time is 1-2 minutes
  • the pressure is 12-18Mpa.
  • the compatibilizer is selected from one or a mixture of ethylene-acrylate-maleic anhydride terpolymer, linear low-density polyethylene grafted maleic anhydride, and ethylene-octene copolymer grafted maleic anhydride.
  • the processing aids are selected from one or a mixture of low molecular weight esters, metal soaps, stearic acid complex esters, amides and the like.
  • the dispersant is selected from one or a combination of hydroxypropyl methyl cellulose (HPMC) and polyacrylamide (PAM).
  • HPMC hydroxypropyl methyl cellulose
  • PAM polyacrylamide
  • the toughening agent is one or two or three of ethylene-acrylic acid copolymer, ethylene-vinyl acetate copolymer, and high-density ethylene.
  • the prepared nylon thread has good toughness and rigidity, and has the advantages of simple flow, continuous flow, high production efficiency and stable product quality.
  • Figure 1 is a schematic diagram of the structure of the screw extruder of the present invention.
  • the multi-kilogram knotless preparation process of the present invention includes the following steps:
  • the raw materials include the following components by mass: 100 parts of nylon 6 chips, 120 parts of nylon 66 chips, 5 parts of compatibilizer, 40 parts of toughening agent, 1 part of auxiliary agent, 1 part of dispersant, and The above raw materials are mixed;
  • Drying add the mixed raw materials to the dryer or continuous drying tower for drying, the drying temperature is 120°C, the drying time is 4 hours, the drying vacuum is -0.08MPa, and the moisture content of the slice is 800ppm;
  • the dried raw material is extruded and melted with a screw extruder and then spun, the spinning melt temperature is 180-220°C, and the temperature fluctuation of the spinning melt is controlled at ⁇ 2°C.
  • Pressure melting the temperature in the first zone is 190-200°C, the temperature in the second zone is 188-202°C, the temperature in the third zone is 190-205°C, and the temperature in the fourth zone is 185-199°C;
  • a side blowing device After spinning, a side blowing device is installed in the cooling tunnel for cooling.
  • the side blowing speed is 0.5 meters per second, the side blowing temperature is 22°C, and the wind humidity is 70%;
  • Oiling, spinning cluster oiling the concentration of the oiling agent is 13%, the oiling rate of the oiling agent: 0.85%, and the pressure regulating range is 1 kg;
  • the screw extruder includes a frame, an extrusion device is arranged on the frame, and a cooling device is arranged outside the extrusion device.
  • the extrusion device includes a barrel, a screw and an extrusion die, and a feed port is provided on the barrel.
  • the screw is arranged inside the barrel, the cooling device is arranged on the outside of the barrel, and the cooling device is a multi-section spiral cooling water channel wound on the outside of the barrel. The two ends of the cooling water channel are the water inlet and the water outlet respectively.
  • the outside of the extruder barrel is cooled in sections according to the internal partitions to ensure that the temperature of each partition meets the set requirements.
  • the spiral cooling water pipes provide uniform cooling and good results.
  • the flange temperature is 200-230°C
  • the box temperature is 190-205°C
  • the metering pump speed is 14-15 revolutions per minute.
  • the extrusion temperature is 210-240°C
  • the rotation speed is 200-260rpm
  • the temperature range of each zone of the extrusion process is 200-260°C
  • the residence time is 1-2 minutes
  • the pressure is 12-18Mpa.
  • the compatibilizer is selected from one or a mixture of ethylene-acrylate-maleic anhydride terpolymer, linear low-density polyethylene grafted maleic anhydride, and ethylene-octene copolymer grafted maleic anhydride.
  • the processing aids are selected from one or a mixture of low molecular weight esters, metal soaps, stearic acid complex esters, amides and the like.
  • the dispersant is selected from one or a combination of hydroxypropyl methyl cellulose (HPMC) and polyacrylamide (PAM).
  • HPMC hydroxypropyl methyl cellulose
  • PAM polyacrylamide
  • the toughening agent is one or two or three of ethylene-acrylic acid copolymer, ethylene-vinyl acetate copolymer, and high-density ethylene.
  • the prepared nylon thread has good toughness and rigidity, and has the advantages of simple flow, continuous flow, high production efficiency and stable product quality.
  • Nylon 6/66 copolymer chip is an in-situ polymerized modified nylon chip with good mechanical properties, strong abrasion resistance, low melting point and plasticizing properties. It is extremely versatile and can be used to make fishing lines. Fishing line made of nylon 6 monofilament accounts for more than 50% of the total. Nylon 6/66 copolymer chips are ideal spinning raw materials for modern fishing lines.
  • nylon 6 and nylon 66 materials are produced by using nylon 6 and nylon 66 materials in a certain ratio by in-situ polymerization technology.
  • the nylon 6 monofilament fishing line spun with it has a thinner diameter, softer, more wear-resistant, and more convenient throwing.
  • Nodules have better strength, more water resistance, and more suitable for various types of fishing line knots.
  • fluorocarbon wires and PE wires they have better ductility, provide better cushioning, and are extremely high
  • the ratio of the nodule tension to the linear tension, the dyeing performance is excellent, and it is easier to dye various colors.

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  • Engineering & Computer Science (AREA)
  • Textile Engineering (AREA)
  • Mechanical Engineering (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Manufacturing & Machinery (AREA)
  • Artificial Filaments (AREA)

Abstract

A multi-kilogram-level knotless thread preparation process, comprising the following steps: mixing raw materials, drying, extruding and melting the dried raw materials by a screw extruder, spinning, cooling, oiling, winding and forming. Nylon threads prepared by the multi-kilogram-level knotless thread preparation process have advantages of good toughness and rigidity, simple and continuous process, high production efficiency, and stable product quality.

Description

多公斤级无结线制备工艺Multi-kilogram knotless wire preparation process 技术领域Technical field
本发明涉及纤维加工技术领域,特别涉及多公斤级无结线制备工艺。The invention relates to the technical field of fiber processing, in particular to a multi-kilogram-level knotless thread preparation process.
背景技术Background technique
钓鱼线就是钓鱼时鱼竿上所挂的线,类似于蜘蛛吐出来的丝,很细却很结实。钓鱼线是生活中常用到的一种线。钓鱼线不止是钓鱼用的,然而我们生活中绑东西也会用得到。The fishing line is the line that hangs on the fishing rod when fishing, similar to the silk spit out by a spider, very thin but very strong. Fishing line is a kind of line commonly used in life. Fishing line is not only used for fishing, but we can also use tied things in our lives.
尼龙线又名传统线,四色线。尼龙线的制造过程,一般是取树脂加工抽丝而成(传统线)并于成品上添加其他素材如颜色(四色线),其特性是具有较佳的延展性和弹性。Nylon thread is also known as traditional thread, four-color thread. The manufacturing process of nylon thread is generally made of resin processing and spinning (traditional thread) and adding other materials such as color (four-color thread) to the finished product. Its characteristic is that it has better ductility and elasticity.
尼龙钓鱼线基本规格有两种:一种是欧美国家用「磅」定的规格,例如十磅的线,它的最大拉力能够承受到十磅的重量;另外一种是日本制造的钓鱼线,通常都以「号」数规格区分,还有欧洲制造的。There are two basic specifications of nylon fishing line: one is the specifications set by European and American countries with "pounds", such as a ten-pound line, which can withstand a maximum tensile force of ten pounds; the other is a fishing line made in Japan. They are usually distinguished by "number" and specifications, and there are European ones.
原理和磅数的立意相同,大约一号的线,它的最大拉力能够承受一公斤的重量,作为在水中拉鱼的一种标准依据。The principle is the same as the concept of the number of pounds. The maximum pulling force of a line of about one kilogram can be used as a standard basis for pulling fish in the water.
以尼龙6单丝为主的线越来越不能满足人们多领域全方位的使用,性能上仍有很大提升的空间。The thread based on nylon 6 monofilament is increasingly unable to meet people's comprehensive use in many fields, and there is still much room for improvement in performance.
发明内容Summary of the invention
本发明的目的是提供一种多公斤级无结线制备工艺,采用尼龙6和尼龙66两种材料按照一定的比例制备,性能更加优越。The purpose of the present invention is to provide a multi-kilogram-level knotless thread preparation process, which adopts nylon 6 and nylon 66 materials in a certain ratio and is prepared with superior performance.
为实现上述目的,本发明提供了多公斤级无结线制备工艺,包括以下步骤:In order to achieve the above objective, the present invention provides a multi-kilogram-level knotless preparation process, which includes the following steps:
1、原料混合,原料包括以下质量份数的组分:尼龙6切片100份,尼龙66切片100-150份,相容剂2-10份,增韧剂20-50份,助剂0.8-1份,分散剂0.8-1份,将以上原料混合;1. The raw materials are mixed. The raw materials include the following components by mass: 100 parts of nylon 6 chips, 100-150 parts of nylon 66 chips, 2-10 parts of compatibilizer, 20-50 parts of toughening agent, 0.8-1 parts of auxiliary Parts, 0.8-1 part of dispersant, mix the above raw materials;
2、干燥,将混合原料加入干燥机或连续干燥塔进行干燥,干燥温度110-125℃,干燥时间3.5-4.5小时,干燥真空度为-0.07~-0.09MPa,干燥至切片的水分含量为750-900ppm;2. Drying, add the mixed raw materials to the dryer or continuous drying tower for drying, the drying temperature is 110-125℃, the drying time is 3.5-4.5 hours, the drying vacuum degree is -0.07~-0.09MPa, and the moisture content of the slice is 750 -900ppm;
3、将干燥后的原料用螺杆挤压机进行挤压熔融后纺丝,纺丝熔体温度180-220℃,纺丝熔体温度波动控制在±2℃,所述螺杆挤压机的挤压熔融,一区温度为190-200℃,二区温度为188-202℃,三区温度为190-205℃,四区温度为185-199℃;3. The dried raw material is extruded and melted with a screw extruder and then spun, the spinning melt temperature is 180-220°C, and the temperature fluctuation of the spinning melt is controlled at ±2°C. Pressure melting, the temperature in the first zone is 190-200℃, the temperature in the second zone is 188-202℃, the temperature in the third zone is 190-205℃, and the temperature in the fourth zone is 185-199℃;
4、冷却,纺丝后冷却甬道中设置侧吹风装置进行冷却,侧吹风速度0.5米每秒,侧吹风风温度19-27℃,风的湿度为62-75%;4. Cooling. After spinning, a side blowing device is installed in the cooling tunnel for cooling. The side blowing speed is 0.5 meters per second, the side blowing temperature is 19-27°C, and the wind humidity is 62-75%;
5、上油,纺丝集束上油,油剂浓度为12.8-14.4%,油剂上油率:0.75-0.95%,调压范围在0.32-2.1公斤;5. Oiling, spinning cluster oiling, the concentration of the oiling agent is 12.8-14.4%, the oiling rate of the oiling agent: 0.75-0.95%, and the pressure regulating range is 0.32-2.1 kg;
6、卷绕成型,上导丝盘频率:61-76HZ,卷绕速度:979-995米/分钟,下导丝盘频率:61-77HZ,摩擦辊频率:68-74HZ,往复横动频率:57-66HZ。6. Winding forming, upper godet frequency: 61-76HZ, winding speed: 979-995 m/min, lower godet frequency: 61-77HZ, friction roller frequency: 68-74HZ, traverse frequency: 57-66HZ.
所述螺杆挤出机包括机架,在机架上设置挤出装置,在挤出装置外部设置冷却装置,挤出装置包括料筒、螺杆及挤出模头,在料筒上设置进料口,螺杆设置在料筒内部,冷却装置设置在料筒外侧,冷却装置为多段缠绕在料筒外侧的螺旋形冷却水通道,冷却水通道两端分别为进水端和出水端。The screw extruder includes a frame, an extrusion device is arranged on the frame, and a cooling device is arranged outside the extrusion device. The extrusion device includes a barrel, a screw and an extrusion die, and a feed port is provided on the barrel. The screw is arranged inside the barrel, the cooling device is arranged on the outside of the barrel, and the cooling device is a multi-section spiral cooling water channel wound on the outside of the barrel. The two ends of the cooling water channel are the water inlet and the water outlet respectively.
对挤出机料筒外侧根据内部分区进行分段冷却,保证各个分区的温度达到设定要求,螺旋状的冷却水管,冷却均匀,并且效果好。The outside of the extruder barrel is cooled in sections according to the internal partitions to ensure that the temperature of each partition meets the set requirements. The spiral cooling water pipes provide uniform cooling and good results.
其中螺杆挤压机挤压熔融时,法兰温度为200-230℃,箱体温度为190-205℃,计量泵转速为14-15转每分钟。挤出温度为210-240℃,转速为200-260rpm,其挤出工艺各区温度范围为200~260℃,停留时间1-2分钟,压力为12-18Mpa。When the screw extruder is extruding and melting, the flange temperature is 200-230°C, the box temperature is 190-205°C, and the metering pump speed is 14-15 revolutions per minute. The extrusion temperature is 210-240°C, the rotation speed is 200-260rpm, the temperature range of each zone of the extrusion process is 200-260°C, the residence time is 1-2 minutes, and the pressure is 12-18Mpa.
所述相容剂选自乙烯-丙烯酸酯-马来酸酐三元共聚物、线性低密度聚乙烯接枝马来酸酐、乙烯-辛烯共聚物接枝马来酸酐等的一种或其混合物。The compatibilizer is selected from one or a mixture of ethylene-acrylate-maleic anhydride terpolymer, linear low-density polyethylene grafted maleic anhydride, and ethylene-octene copolymer grafted maleic anhydride.
加工助剂选自低分子酯类、金属皂类、硬脂酸复合酯类、酰胺类等中的一种或几种的混合物。The processing aids are selected from one or a mixture of low molecular weight esters, metal soaps, stearic acid complex esters, amides and the like.
分散剂选自羟丙基甲基纤维素(HPMC),聚丙烯酰胺(PAM)中的一种或者组合物。The dispersant is selected from one or a combination of hydroxypropyl methyl cellulose (HPMC) and polyacrylamide (PAM).
增韧剂为乙烯-丙烯酸共聚物、乙烯-醋酸乙烯共聚物、高密度乙烯中的一种或两种或三种。The toughening agent is one or two or three of ethylene-acrylic acid copolymer, ethylene-vinyl acetate copolymer, and high-density ethylene.
本发明的多公斤级无结线制备工艺,制备的尼龙线具有较好的韧性和刚度,具有流程简单、连续、生产效率高、产品质量稳定的优点。In the multi-kilogram knotless thread preparation process of the present invention, the prepared nylon thread has good toughness and rigidity, and has the advantages of simple flow, continuous flow, high production efficiency and stable product quality.
附图说明Description of the drawings
图1是本发明螺杆挤出机的结构示意图图;Figure 1 is a schematic diagram of the structure of the screw extruder of the present invention;
具体实施方式detailed description
下面结合附图详细说明本发明的优选技术方案。The preferred technical solutions of the present invention will be described in detail below with reference to the accompanying drawings.
本发明的多公斤级无结线制备工艺,包括以下步骤:The multi-kilogram knotless preparation process of the present invention includes the following steps:
1、原料混合,原料包括以下质量份数的组分:尼龙6切片100份,尼龙66切片120份,相容剂5份,增韧剂40份,助剂1份,分散剂1份,将以上原料混合;1. Mixing of raw materials, the raw materials include the following components by mass: 100 parts of nylon 6 chips, 120 parts of nylon 66 chips, 5 parts of compatibilizer, 40 parts of toughening agent, 1 part of auxiliary agent, 1 part of dispersant, and The above raw materials are mixed;
2、干燥,将混合原料加入干燥机或连续干燥塔进行干燥,干燥温度120℃,干燥时间4小时,干燥真空度为-0.08MPa,干燥至切片的水分含量为800ppm;2. Drying, add the mixed raw materials to the dryer or continuous drying tower for drying, the drying temperature is 120°C, the drying time is 4 hours, the drying vacuum is -0.08MPa, and the moisture content of the slice is 800ppm;
3、将干燥后的原料用螺杆挤压机进行挤压熔融后纺丝,纺丝熔体温度180-220℃,纺丝熔体温度波动控制在±2℃,所述螺杆挤压机的挤压熔融,一区温度为190-200℃,二区温度为188-202℃,三区温度为190-205℃,四区温度为185-199℃;3. The dried raw material is extruded and melted with a screw extruder and then spun, the spinning melt temperature is 180-220°C, and the temperature fluctuation of the spinning melt is controlled at ±2°C. Pressure melting, the temperature in the first zone is 190-200℃, the temperature in the second zone is 188-202℃, the temperature in the third zone is 190-205℃, and the temperature in the fourth zone is 185-199℃;
4、冷却,纺丝后冷却甬道中设置侧吹风装置进行冷却,侧吹风速度0.5米每秒,侧吹风风温度22℃,风的湿度为70%;4. Cooling. After spinning, a side blowing device is installed in the cooling tunnel for cooling. The side blowing speed is 0.5 meters per second, the side blowing temperature is 22°C, and the wind humidity is 70%;
5、上油,纺丝集束上油,油剂浓度为13%,油剂上油率:0.85%,调压范围在1公斤;5. Oiling, spinning cluster oiling, the concentration of the oiling agent is 13%, the oiling rate of the oiling agent: 0.85%, and the pressure regulating range is 1 kg;
6、卷绕成型,上导丝盘频率:61-76HZ,卷绕速度:979-995米/分钟,下导丝盘频率:61-77HZ,摩擦辊频率:68-74HZ,往复横动频率:57-66HZ。6. Winding forming, upper godet frequency: 61-76HZ, winding speed: 979-995 m/min, lower godet frequency: 61-77HZ, friction roller frequency: 68-74HZ, traverse frequency: 57-66HZ.
所述螺杆挤出机包括机架,在机架上设置挤出装置,在挤出装置外部设置冷却装置,挤出装置包括料筒、螺杆及挤出模头,在料筒上设置进料口,螺杆设置在料筒内部,冷却装置设置在料筒外侧,冷却装置为多段缠绕在料筒外侧的螺旋形冷却水通道,冷却水通道两端分别为进水端和出水端。The screw extruder includes a frame, an extrusion device is arranged on the frame, and a cooling device is arranged outside the extrusion device. The extrusion device includes a barrel, a screw and an extrusion die, and a feed port is provided on the barrel. The screw is arranged inside the barrel, the cooling device is arranged on the outside of the barrel, and the cooling device is a multi-section spiral cooling water channel wound on the outside of the barrel. The two ends of the cooling water channel are the water inlet and the water outlet respectively.
对挤出机料筒外侧根据内部分区进行分段冷却,保证各个分区的温度达到设定要求,螺旋状的冷却水管,冷却均匀,并且效果好。The outside of the extruder barrel is cooled in sections according to the internal partitions to ensure that the temperature of each partition meets the set requirements. The spiral cooling water pipes provide uniform cooling and good results.
其中螺杆挤压机挤压熔融时,法兰温度为200-230℃,箱体温度为190-205℃,计量泵转速为14-15转每分钟。挤出温度为210-240℃,转速为200-260rpm,其挤出工艺各区温度范围为200~260℃,停留时间1-2分钟,压力为12-18Mpa。When the screw extruder is extruding and melting, the flange temperature is 200-230°C, the box temperature is 190-205°C, and the metering pump speed is 14-15 revolutions per minute. The extrusion temperature is 210-240°C, the rotation speed is 200-260rpm, the temperature range of each zone of the extrusion process is 200-260°C, the residence time is 1-2 minutes, and the pressure is 12-18Mpa.
所述相容剂选自乙烯-丙烯酸酯-马来酸酐三元共聚物、线性低密度聚乙烯接枝马来酸酐、乙烯-辛烯共聚物接枝马来酸酐等的一种或其混合物。The compatibilizer is selected from one or a mixture of ethylene-acrylate-maleic anhydride terpolymer, linear low-density polyethylene grafted maleic anhydride, and ethylene-octene copolymer grafted maleic anhydride.
加工助剂选自低分子酯类、金属皂类、硬脂酸复合酯类、酰胺类等中的一种或几种的混合物。The processing aids are selected from one or a mixture of low molecular weight esters, metal soaps, stearic acid complex esters, amides and the like.
分散剂选自羟丙基甲基纤维素(HPMC),聚丙烯酰胺(PAM)中的一种或者组合物。The dispersant is selected from one or a combination of hydroxypropyl methyl cellulose (HPMC) and polyacrylamide (PAM).
增韧剂为乙烯-丙烯酸共聚物、乙烯-醋酸乙烯共聚物、高密度乙烯中的一种或两种或三种。The toughening agent is one or two or three of ethylene-acrylic acid copolymer, ethylene-vinyl acetate copolymer, and high-density ethylene.
本发明的多公斤级无结线制备工艺,制备的尼龙线具有较好的韧性和刚度,具有流程简单、连续、生产效率高、产品质量稳定的优点。In the multi-kilogram knotless thread preparation process of the present invention, the prepared nylon thread has good toughness and rigidity, and has the advantages of simple flow, continuous flow, high production efficiency and stable product quality.
尼龙6/66共聚切片是一款力学性能好,耐磨性强,熔点低,塑化性能的原位聚合改性尼龙切片,用途极为广泛,可用来制作钓鱼线。以尼龙6单丝制作的钓鱼线占到总量的50%以上,尼龙6/66共聚切片是现代钓鱼线理想的纺丝原材料。Nylon 6/66 copolymer chip is an in-situ polymerized modified nylon chip with good mechanical properties, strong abrasion resistance, low melting point and plasticizing properties. It is extremely versatile and can be used to make fishing lines. Fishing line made of nylon 6 monofilament accounts for more than 50% of the total. Nylon 6/66 copolymer chips are ideal spinning raw materials for modern fishing lines.
它采用尼龙6和尼龙66两种材料按照一定的比例,采用原位聚合技术生产出来的,用它纺制的尼龙6单丝钓鱼线直径更细,更柔软,更耐磨,更方便抛投,结节强度更佳,更 耐水浸,更适合打各种类型的鱼线结,与氟碳线与PE线相比具有更好的延展性,能提供更好的缓冲作用,而且具有极高的结节拉力与直线拉力比值,染色性能优良,更容易染成各种颜色。It is produced by using nylon 6 and nylon 66 materials in a certain ratio by in-situ polymerization technology. The nylon 6 monofilament fishing line spun with it has a thinner diameter, softer, more wear-resistant, and more convenient throwing. , Nodules have better strength, more water resistance, and more suitable for various types of fishing line knots. Compared with fluorocarbon wires and PE wires, they have better ductility, provide better cushioning, and are extremely high The ratio of the nodule tension to the linear tension, the dyeing performance is excellent, and it is easier to dye various colors.

Claims (2)

  1. 多公斤级无结线制备工艺,其特征在于包括以下步骤:The multi-kilogram knotless wire preparation process is characterized by including the following steps:
    1)原料混合,原料包括以下质量份数的组分:尼龙6切片100份,尼龙66切片100-150份,相容剂2-10份,增韧剂20-50份,助剂0.8-1份,分散剂0.8-1份,将以上原料混合;1) Mixing of raw materials, the raw materials include the following parts by mass: 100 parts of nylon 6 chips, 100-150 parts of nylon 66 chips, 2-10 parts of compatibilizer, 20-50 parts of toughening agent, 0.8-1 parts of auxiliary Parts, 0.8-1 part of dispersant, mix the above raw materials;
    2)干燥,将混合原料加入干燥机或连续干燥塔进行干燥,干燥温度110-125℃,干燥时间3.5-4.5小时,干燥真空度为-0.07~-0.09MPa,干燥至切片的水分含量为750-900ppm;2) Drying, add the mixed raw materials to the dryer or continuous drying tower for drying, the drying temperature is 110-125℃, the drying time is 3.5-4.5 hours, the drying vacuum is -0.07~-0.09MPa, and the moisture content of the slice is 750 -900ppm;
    3)将干燥后的原料用螺杆挤压机进行挤压熔融后纺丝,纺丝熔体温度180-220℃,纺丝熔体温度波动控制在±2℃,所述螺杆挤压机的挤压熔融,一区温度为190-200℃,二区温度为188-202℃,三区温度为190-205℃,四区温度为185-199℃;3) The dried raw material is extruded and melted with a screw extruder and then spun, the spinning melt temperature is 180-220°C, and the spinning melt temperature fluctuation is controlled at ±2°C. The extrusion of the screw extruder Pressure melting, the temperature in the first zone is 190-200℃, the temperature in the second zone is 188-202℃, the temperature in the third zone is 190-205℃, and the temperature in the fourth zone is 185-199℃;
    4)冷却,纺丝后冷却甬道中设置侧吹风装置进行冷却,侧吹风速度0.5米每秒,侧吹风风温度19-27℃,风的湿度为62-75%;4) Cooling: After spinning, a side blowing device is installed in the cooling tunnel for cooling. The side blowing speed is 0.5 meters per second, the side blowing temperature is 19-27°C, and the humidity of the wind is 62-75%;
    5)上油,纺丝集束上油,油剂浓度为12.8-14.4%,油剂上油率:0.75-0.95%,调压范围在0.32-2.1公斤;5) Oiling, spinning cluster oiling, the concentration of the oiling agent is 12.8-14.4%, the oiling rate of the oiling agent: 0.75-0.95%, and the pressure regulating range is 0.32-2.1 kg;
    6)卷绕成型,上导丝盘频率:61-76HZ,卷绕速度:979-995米/分钟,下导丝盘频率:61-77HZ,摩擦辊频率:68-74HZ,往复横动频率:57-66HZ。6) Winding forming, upper godet frequency: 61-76HZ, winding speed: 979-995 m/min, lower godet frequency: 61-77HZ, friction roller frequency: 68-74HZ, traverse frequency: 57-66HZ.
  2. 如权利要求1所述的多公斤级无结线制备工艺,其特征在于:所述螺杆挤出机包括机架,在机架上设置挤出装置,在挤出装置外部设置冷却装置,挤出装置包括料筒、螺杆及挤出模头,在料筒上设置进料口,螺杆设置在料筒内部,冷却装置设置在料筒外侧,冷却装置为多段缠绕在料筒外侧的螺旋形冷却水通道,冷却水通道两端分别为进水端和出水端。The multi-kilogram knotless wire preparation process according to claim 1, wherein the screw extruder includes a frame, an extrusion device is arranged on the frame, and a cooling device is arranged outside the extrusion device, and the extruder The device includes a barrel, a screw and an extrusion die. The barrel is provided with a feed port, the screw is set inside the barrel, and the cooling device is set on the outside of the barrel. The cooling device is multi-section spiral cooling water wound on the outside of the barrel. The two ends of the channel and the cooling water channel are the water inlet and the water outlet respectively.
PCT/CN2019/087566 2019-02-18 2019-05-20 Multi-kilogram-level knotless thread preparation process WO2020168642A1 (en)

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Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003250408A (en) * 2002-03-06 2003-09-09 Toray Monofilament Co Ltd Fishing line and method for producing the same
CN202415811U (en) * 2011-12-31 2012-09-05 杭州帝凯工业布有限公司 High-strength nylon 6 industrial filament
CN108866704A (en) * 2018-07-28 2018-11-23 安徽省义顺渔网渔具有限公司 A kind of ageing-resistant fishing lines of high-strength corrosion-resisting
CN109234841A (en) * 2018-09-11 2019-01-18 厦门市富众渔具有限公司 A kind of tuna fishline and preparation method thereof
CN109706565A (en) * 2019-02-18 2019-05-03 海安县中祥线业有限公司 More feather weight are without tie lines preparation process

Family Cites Families (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE19648436A1 (en) * 1996-11-22 1998-05-28 Basf Ag Longlines
AR011096A1 (en) * 1997-03-20 2000-08-02 Rhodia Filtec Ag METHOD FOR THE MANUFACTURE OF ROUND MONOFILAMENTS AND MONOFILAMENT FOR TECHNICAL FABRIC
CN102090382B (en) * 2010-12-17 2012-05-30 东莞市协永福实业有限公司 Method for improving strength of nylon fishing line after being knotted
CN104562273A (en) * 2014-06-25 2015-04-29 巢湖市荷花渔网有限公司 Method for processing fishing net thread by nylon
CN204172324U (en) * 2014-09-11 2015-02-25 东莞市金彩色母有限公司 A kind of look female extrusion device
CN104195667B (en) * 2014-09-15 2016-01-13 马海燕 Athletic type nylon setline and production method thereof
CN106119998A (en) * 2016-08-26 2016-11-16 山东合信科技股份有限公司 A kind of spinning technique of PA66 undrawn yarn

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003250408A (en) * 2002-03-06 2003-09-09 Toray Monofilament Co Ltd Fishing line and method for producing the same
CN202415811U (en) * 2011-12-31 2012-09-05 杭州帝凯工业布有限公司 High-strength nylon 6 industrial filament
CN108866704A (en) * 2018-07-28 2018-11-23 安徽省义顺渔网渔具有限公司 A kind of ageing-resistant fishing lines of high-strength corrosion-resisting
CN109234841A (en) * 2018-09-11 2019-01-18 厦门市富众渔具有限公司 A kind of tuna fishline and preparation method thereof
CN109706565A (en) * 2019-02-18 2019-05-03 海安县中祥线业有限公司 More feather weight are without tie lines preparation process

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